Double effect salt-water still



July 4, 1950 w. H. THOMPSON DOUBLE EFFECT 'SALT WATER STILL 6 Sheets-Sheet 1 Filed NOV. 5, 1946 3nventor u lLL/Alf hf 77/0MPJo/v 3!! $7! 0 dttorneg y 1950 w. THOMPSON I 2,513,901

I v 7 DOUBLE EFFECT SALT WATER STILL y 1950 w. H. THOMPSON 2,513,901

DOUBLE EFFECT SALT WATER STILL Filed Nov. 5, 1946 6 Sheets-Sheet 3 attorney July 4, 1950 w. H. THOMPSON DOUBLE EFFECT SALT WATER s'rm.

6 Sheets-Sheet 4 Filed Nov. 5, 1946 Jnventor M1 4 44/1 fi o/rem (Ittorneg July 4, 1950 w. H. THOMPSON 2,513,901 DOUBLE EFFECT SALT WATER STILL Filed Nov. 5, 1946 6 Sheets-Sheet 5 Q\- J\I\ b s Q MK Q Ihmentor (lttomeg w. H. THOMPSON 2,513,901

DOUBLE EFFECT SALT WATER STILL 6 Sheets-Sheet 6 Filed NOV. 5, 1946 Patented July 4, 1950 UNIT-El) STATES rATENT OFFICE DOUBLE EFFECT SALT-WATER STILL -William H. gThompson, Chatham, N. J., assignor to Davis Engineering Corporation, Elizabeth,

I N. IL, a corporation of Delaware Application November 5, 1946, Serial No. 707374 The invention herein disclosedrela'tes to a distillation system that is particularly suitable for supplying distilled Water for human consumption.

The foregoing objects and certain advantages that will hereinafter appear are realized in the embodiment of the inventidnillustrated in the accompanying drawing and described in detail below, from which de'scription' a clearer understanding of the-invention maybe had. 7

The drawings include: 7

"Fig. 1 which is a *front elevation of a distillation plant embodying the invention;

Fig. 2 which is a plan of the same;

Fig. '3

same; I 7 I Fig. 4 which is a right, side elevation thereof;

Fig. 5 which is a transverse section of the-same taken on the line '5-50'f 'Fig. 1; and

6 which is apiping diagram'of the system.

As illustrated in Figs. I -5 of 'the'drawings, the distillation plant, selected for the purposes of illustrating a preferred embodiment of the in vention, is "arranged :as a unit. It is adapted to be assembled as a' unitiat the factory and installed as a unit aboards'hip. When installed, the steam and water connections are made to the appropriate lines and the unit is ready for operation.

To this end all of-the apparatus making up the distillation plant is counted -upon and supported by abase frame desighatedgenera lly'by the char acter A. Upon this ?base frame, there are the necessary supports'for the various com'ponentsof the distillation system. In general these component parts of the include a vapor feed water heater B'; a combined after con'denser and external feed water heater [6; a double effect evaporator D; a condenser E; 'andthe necessary piping, valves, controls *and pumps for the interconnection of these compcnent'parts'and-thecontrol and flow of steam and water; i

The base frame A consists :of-a'rect'angula frame made up of four channel iirons', welded to- Which is a left. side elevation of the thereto, there are several I-beams such 5 Claims. (Cl. 202- 174) gether; -a front channel iron I, a rear channel iron 2, and side channel irons 3 and 4. Inter mediatethe-side channel:irona'eXtending between I the front and rear channel irons and welded as the I-beam 5 (Fig. '1). Uprights and cross beams, ap-

propriately-located and extending fromthe frame may be'u'se'd to support certain 'of the'component parts of theiplan't. These-havebeen'omittedfrom the drawing in the interest of a clearer illustration of the distillation plant.

The double efiect evaporator D is the largest component part of the :plant and :provides the vapor which is condensed by thecondenser E to provide distillate that is suitable for human use and consumption. Thisdouble'efiectevaporator, which is comprehended Within this invention,

'comprisesxtwo -evaporators mounted within a single, "cylindrical shell 6. The shell '6 is mounted vertically upon the base, frame member A and is closed at its ends by convexed top and bottom members 1 and 8. rnternally th'e shell 6 is divided into t'wo'separate compartments 9 and Ill (Figs. 2, 5 an'd'6-) by spaced, transverse plates l l and 12, weldedto the sidesbottom and-top of the shell. Each compartment constitutes a separate and distinct evaporator.

- Within 'the compartment 10, which constitutes the *first effect evaporator, there are -a plurality of vertically arranged, helical coils l3 (Figs. 1, 5 and-6) connected at their'upper and lower ends, and supported by upper and lower manifolds M and I5. The manifolds extend from a door It, which in the normal, operating position closes an opening l1 through the shell and opening to the :chamber .10." The door it is-supporte'd by a pivotally mounted 'arm 18 -:(Fig. 5);.pivoted-at l9.

' The coils-l3 are so arranged (Fig. 5') that"the door l6 may befiswungopen (asshownin broken lines (in Fig. 5) ,and the coilswill move out of the chamber Hi to such an extent as to leave the opening [1 free. Thus, upon disconnecting the pipe "connections; hereinai'ter described, the door [6 may beopened to exposedthecoils t3 and the interior of the compartment H), for inspection and cleaning. In like =manner,-and for the same purpose-coils-ZO are mounted betweenmanifolds extending from a door 2| that closesan opening- 22 toethe compartmentfl.

Each j'compartment is provided coveredjobservation opening 2 5. Similarly,--the with a visual thermometer, pressure guage and observation opening. The compartment 'Hl (Fig. 1 has a pressure guage '23, a thermometer -24;-and a glasstically, (Fig. 2) sufiiciently to come within the confines partment at the particular elevation indicated, to permit observation of the foaming and priming of the water being evaporated.

The vapor feed water heater B is mounted verat the rear of the shell 6, and to the left of the base frame. Thisfeed water heater includes a cylindrical shell 29 and the usual end heads. Within the shell there are straight tubes rolled into tube sheets in a mannerv well known in the art and indicated diagrammatically at 39, in Fig. 6. I 7

The combined after condenser and feed-water inlet 49 of the tubes 38 of the condenser E. More sea water is required to condense and cool the vapors delivered to the condenser than is required by the distillation plant. For this reason, the outlet 4! of the coil 38 is connected to a T- fitting 42. Through this T-fitting the outlet 4! of the tubes 38 is connected in common to an overboard discharge 4-3 and a pipe 44. which constitutes a passage for the evaporator feed water. The feed water pipe 44 is connected through a three way, two port plug valve 45 (Fig. 6) to the inlet end of an evaporator, feed pump Mi, driven by an electric motor 41. One side of the valve heater C also consists of a cylindrical shell 3i mounted vertical, behind I!) of the double effect evaporator D.

and adjacent the com- 45 is connected through a connection 49, to the inner bottom reserve feed tanks of the ship to which, through the valve 45, the feed pump may be connected under. adverse conditions. Thus,

I .thereare two sources for feeding the evaporators,

The shell 3| is closed at each end by the usual removable heads 32 and 33 (Figs. 4 and 6). Within the shell (Fig. 6), there is a tudinal partition 34 extending from the upper head to a point adjacent the lower head 33. Two,

or a multiple thereof, sets of tubes indicated diagrammatically at 35and'36 in Fig. 6 are contained in the shell, equally' divided on each side of the partition 34 and connected together in series. The condenser E is mounted horizontally to the left of and adjacent the top of the double effect evaporator D. This condenser consists of a cylindrical shell 31 within which there are two separate (Fig. 6) passages or sets of tubes 38 and 39. The tubes, as is been herein mentioned, have outlet connections'and do not communicate the shell, except that they are in heat-transfer relation to any fluid within'the shell.

separate inlet and diametrical, longithe case where tubes have With In addition to the above described component:

parts of the unitarydistillation plant of this invention, there is comprehended within the system of the invention, the piping of these parts, one to the other, to obtain a particular flow of fluids, and the pumps and control mechanism for affecting the desired results. Generally speaking, the water tobe distilled flows through the tubes of the condenser E to condense the vapors in the shell; the tubes of the vapor feed water heater B; the tubes of the combined after condenser and feed water heater C; the shell of thefirst effect evaporator, and the shell of the second'effect evaporator, both of which constitute the double effect evaporator D; and from the'second effect evaporator the concentrated water is pumped overboard. Steam from the exhaust steam supply of the ship is delivered to the tubes of the first effect evaporator and also to the combined vapor feed watef'heater B and the' majorpart through the tubesof the'second effect evapo .ratorl' From 'thevapor'feecl water heater B and the tubes of: the second e'ff'e'ct evaporator, these vapors and condensate pass to the shell of the condenser E. I the second effect evaporator (chamber 9) pass to the condenser. The distillate from the condenser is free of all impurities. T

The piping, pump and control arrangement is hereinafter described first in relation to the flow of the' water to be distilled, second in relation to the distillation, third in relation to the heating fluid, and'fourth in relation to the various controls. Sea water, from the saltwater circulating system of the ship is connected to the In addition; vapors formed in:

water directly from the-,sea and the inner bottom reserve tanks of the'ship.

From the pressureor exhaust end of the pump 46, a pipe 49 is connected to a rate of flow meter pump and the rate of flow 50. Intermediate the vent reverse flow, and a high level valve 5| com trolled by a float control52, hereinafter described. From the meter pipe 53 to the inlet tion 55 of the tubes, 39, the sea water passes through a pipe 56 to the inlet end ofthe tubes 39 within the shell 29 of the vaporfeed Water heater B. From the outlet'of the delivered through a pipe 5'! to the inletofthe tubes 36 of the :combined after condenser and external feed water heater C.

The combined after condenser, and external, feed water heatenc operates as a condenser, as. will be hereinafter described, and an additionalfeed water heater. In the latter capacity, itis provided to insure that the water to be distilled will be heated above degrees Fahrenheit. This has been a requirement of the health service and is intended as assurance that all bacteria will be destroyed.

The waterpasses through the tubes 36 and the tubes 35 and through a pipe line 58 to the chamber ll] of the double effect evaporator D. In the line 58, there is connected an aqua switch 59, adjacent the outlet from the tubes 35; a temperature bulb connection 69,'which through a line (if actuates a valve 62, in the steam line (hereinafter described) the globe valve 63, adjacent the inlet to the chamber Within the chamber ili, the water is evaporated and vapors flow through a, pipe 65 to the inlet to the tubes 29 within the compartment 9. From the tubes 20 the vapor and condensate flow through a :pipeSB to the shell of the condenser E. An air vent line 61, connects the outlet end of the tubes 29 and the pipe 66; a valve 31 being interposed therein. In the line 66, adjacent the outlet from the 68, a thermometer 69 and a globe valve 19.

Partof the vapor formed in the chamber ll) passes through a'pipe'llla to the shell-of the vapor feed water heater B wherein it is used to heat the water passing through the tubes 39. The drains from the shell'zof the vapor feed water heater are delivered through a pipe to the shell of the condenser E. Connected in the p pe 101 ja ent the connection to the feed wa-.

swing check valve 59a to ,pre-

50 which provides a continuous, visual indication ,of the rate of flow of water t0v the evaporators, the sea water passes, through connection 54 of the tubes 39 of the condenserEj From the outlet connectubes 39, the water is.

one; hundred and sixty-five- Ill; and a thermometer 64.

tubes 23, there are a salinity cell ter-heater,:there area thermometer .slflcj, ;azsalinity cellflfld and 'awg'lobe fvalve JIM.

Part 'of the Water'delivered to the chamber zIIl flows through :a-nopen :overeflow a arrangement I I such-asdescribed in theiPatentiNo. 2588;7'73, and through-a :pipe 7;'2 ,-.in which'a gate valve 13 is interposed,-to-.the'chamber 9. The highzlevelifioat control 52, connected :inxan equalizer line ":7 5,:communicating with the chamber 8, actuates 'the valve 5| to control theflowof water of :the'evaporators. The high level control is so positioned as to provide 'suflicient water in the chamber 9 which insuresan adequate level in =.the chamber I0 and a continuous discharge through an open overflow 76 in the chamber 9. The overflow" "I6 is constructed as described in thea-foresaid 'U. 6. Patent No. 2,388,773. Excess water passing through the overflow IE5, passes through a pipe TI,'-in which there is a strainer '18, to a pump 19 by which it is pumpedoverboard. There is thus a continuous blow down of. the chambers II! and 9.

A drain connection 80 is connected to the bottom of the chamber IU and a like drain connection 8| extends from the bottom of the chamber 9. These are connected through a three-way, two port cock .82 to the pipe I1 such that the drainage passes through the strainer 18.

Vapor formed .inthe chamber 9 passes through a pipe 83 to theshellof the condenser Thus, the vapors .formed in :thechambers Band I 0 are delivered to the shell of the condenser where they are distilled. Thedis-tillatepasses from the shell of the condenser through a pipe 84, having a flow indicator 85 .of the kind k-nown as a Flowdicator therein, to a distillate pump '86. Just before the pump .86, there is interposed in the pipe 84, a salinity cell 87. The pump delivers the distillate through a pipe 88 to a distilled water reserve feed tank (not shown). In the .pipe 88, there is a three-way solenoid actuated valve 8.9 by means of which the distilled water may be bypassed through a pipe T9!) to the bilge.

The heating fluid is taken from the exhaust steam supply of the ship. This steam, norm-ally at a gauge pressure of ten pounds per square inch, is delivered to an inlet line 3| through aweightloaded reducing valve 92 (Figs. 2, 4 and 6) which may be set at five pounds persquare inch gauge pressure. A pressure gauge '93 is desirably connected in the line between the valve 92 and a relief valve 9 5. The .pipe connects the steam supply to the inlet to the tubes I3 of the chamber IIJ. In the line 91, there is a gate valve 55 and a diaphragm 96 having .an orifice therein of a size to allow justsufficient steam 'therethrough'ior normal.operation. A by-pass line '9! connected 'into the line I! I, at one end before the valve 9'5 and at the other end after the diaphragm 96, has a gate valve 98 therein and a diaphragm 99 having an opening or orifice'therethroug'h for clean operation. Depending upon the operation desired one of the valves "95 or "98 open and the other is closed. A compound gauge I00, 'regis'teringpressure and vacuum, is connected in the line 91 adjacent the connection to the tubes I 3.

From the outlet end of the tubes-I3, 'a pipe I01 isconnected to the shell of the'c'or'nbinedafter condenser and external feed water heater C. Connected in the pipe line I9 I, adjacent the outlet from the tubes -I13,there "are a salinity'cell I02, a thermometer I03 and a globe valve 104. A branch pipe line I65, connected to the pipe '9-I delivers steam directly to the shell of the combined after condenser and feed water heater C.

In this line there is a gate valve I 06 and the-itemperature regulating valve 62. Steamisadmitted to the shell of the after condenser C in'accordance with the temperature of the "feed water leaving the after condenser through the pipe 58.

In addition tocondensing the steam leaving the tubes I3, the after condenser and feed water heater receives the air and vapor discharge from air ejectors Ill! and I08 (Figs. 3 and 8). These air ejectors are provided for removing air from the shell of the condenser. To this end, a pipe I 09 is connected to theejector I08, through a gate valve "H0, and through a branch pipe III to the ejector I01. A valve H2 is provided in the pipe I I I. Steam at high pressure issupplied at a fitting H3 which is connected through a valve I14 and a pipe II5 to the ejector I91, and through a'valve H6 and a, pipe .-I I! to the ejector IOBKFigs. 1,3.and-6). Each ejector I01 and I08 is provided with a, relief valve I I8 and I I9, respectively. The exhaust end of the ejector IN is connected through'a valve I20 to a'pipe I2I connected to the "shell of the after condenser C, and the exhaust from the ejector I08 is .connected through a valve 122 and :a, pipe I23 to the pipe IZI. A pipe I 2-4 connected to the shell of the after condenser aand feed water heater "C delivers the condensate to a pump I25 by which it is pumped to a heater or other apparatus forming no part of this distillation system.

Through the walls of each of the chambers 9 and I0 there is a connection forshock descaling of the tubes therein. The connection to the chamber 9 consists of :a short pipe I26 having a valve I27 therein. "This pipe is connected to the fire system so that cold water "may be directed on the tubes therein. A like pipe I28 having a valve I29 therein is connected through the shell of the chamber II]. By disconnecting the pipe connections to the tubes I3, the door I6 may be opened as above described, and by disconnecting the connections to the tubes 20, the door 2| may be opened.

The salinity cell '81 is electrically connected to control the operations of the three-way, solenoid actuated valve 89. When the salinity of the distillate reaches or exceeds a predetermined valve, the valve 89 is actuated to discharge the distillate to the bilge. When, however, the salinity of the distillate is below the predetermined value, the valve 89 is in position to deliver the distillate to 'thedrinking water and reserve distilled water tanks. The remaining salinity cells are connected to a salinity indicator (not shown but well known in the art). In the event that the salinity of thedistillate -'is such that it is spilled to bilge, the location of the trouble or faulty operation :may be traced by the indications from the several salinity cells.

From the foregoing description of the distillation plant, forming on specific embodiment of the invention, it "will be apparent to those skilled in the art that by this invention, there is provided a distillation system that is unitary in construction; that is adaptable to a compact distillation plant; that is reliable in operation, and that requires 'a'mini'mum of attention and maintenance.

It will be obvious that various changes may be made by those skilled in the art in the details of the embodiment of the inventionillustrate-d in the-drawin and described above within the principle and scope of the invention as expressed in the appended claims.

tally adj acent the vertically adjacent the double effect evaporator,

a combined after-condenser and feed water heater mounted vertically adjacent the double effect evaporator, a condenser mounted horizondouble effect evaporator, connections for delivering steam to th coil in said first effect evaporating chamber, connections for delivering steam to said combined after-condenser and feed water heater, means in said last mentioned connection for controlling the flow of steam to saidvcombined after-condenser and feed fwater heater, control means for said last mentioned means actuated in accordance with the temperature of the water leaving said combined after condenser and feed water heater, connections between the first efiect chamber of said double effect evaporator and the tubes extending into th second effect chamber of said double effect evaporator, a connection between the first effect chamber of said double effect evaporator the said vapor feed water heater, and connections connecting the coil in the second effect chamber of the said double efiect evaporator, the second effect chamber of the said double effect evaporator and the said vapor feed water heater and connections for delivering to the condenser, water in succession to said condenser, saidvapor feed water heater, said combined after condenser and feed water heater and the first effect chamber of said double efiect evaporator.

2. In apparatus for evaporating and distilling liquids, a unitary structure comprising a base frame and supporting elements, a double effect evaporator mounted on the frame and consisting of a vertically mounted cylindrical shell, a diametrical Wall within the shell dividing the shell into a first effect evaporating chamber and a second eifect evaporating chamber, a set of tubes extending into each semi-cylindrical chamher, a steam connection to the tubes extending into the first efiect evaporating chamber, a combined after-condenser and feed water heater including a shell and a coil therein, the combined after-condenser and feed water heater being mounted vertically adjacent said double effect evaporatona connection between the outlet of the tubes in the first efiect chamber of the said double effect evaporator and the shell of the said combined after-condenser and feed water heater, a vapor feed water heater mounted vertically adjacent the said double efiect evaporator, a condenser mounted horizontally adjacent the said double eifect evaporator, a connection for delivering steam directly to the shell of said combined after-condenser and feed water heater, means in said last mentioned connection for controlling the fiow of steam to the shell of said combined after-condenser and Water heater, control means for said last mentioned means actuated inaccordance with the temperature of the water leaving the coil of the said after-condenser and feed water heater, a connection between the first effect chamber of said double efiect evaporator and the inlet to the tubes extending into the second effect chamber of the said double effect evaporator, a connection between the first effect chamber of said double efiect evaporator and the aforesaid vapor feed water heater, connections connecting the outlet of the coil in the second effect chamber of the said double effect evaporator, the second efiect chamber of the said double effect evaporator, and the said vapor feed water heater to the condenser, and connections for delivering water in succession to said condenser, said vapor feed water heater, said combined after condenser and feed water heater and the first effect chamber of said double effect evaporator.

3. In apparatus for evaporating and distilling liquids, a unitary structure comprising a base frame and supporting elements, a double effect evaporator mounted on the frame and consisting of a vertically mounted cylindrical shell, a diametrical wall within the shell dividing the shell into a first effect evaporating chamber and a second effect evaporating chamber, a hingedly mounted door on each side of the diametrical wall, one for each chamber and each door carrying a set of tubes which in the closed positions of the doors extend into the chambers, a steam connection to the tubes extending into the first effect evaporating chamber, a combined'aftercondenser and feed water heater including a shell and a coil therein, the combined after-condenser and feed water heater beingmounted vertically adjacent said double effect evaporator, a connection between the outlet of thetubes in the first effect chamber of the said double effect evaporator and the' shell of the said combined after-condenser and feed water heater, a vapor feed water heater mounted Vertically adjacent the said double effect evaporator, a condenser mounted horizontally adjacent the said double effect evaporator, a connection for delivering steam directly to the shell of said combined after-condenser and feed water heater, means in said last mentioned connection for controlling the flow of steam to the shell of said combined after-condenser and water heater, control means for said last mentioned means actuated in accordance with the temperature of the water leaving the coil of the said after-condenser and feed water heater, a connection between the first effect chamber of said double effect evaporator and the inlet to the tubes extending into the second effect chamber of the said double effect evaporator, a connection between the first effect chamber of said double eifect evaporator and the aforesaid vapor feed water heater, connections connecting the outlet of the coil in the second effect chamber of the said double effect evaporator, the second efiect chamber of the said double effect evaporator, and the said vapor feed water heater to the condenser, and connections for delivering water in succession to said condenser, said vapor feed water heater, said combined after-condenser and feed water heater and the first effect chamber of said double efiect evaporator.

4. In apparatus for evaporating and distilling liquids, a unitary structure comprising a base frame and supporting elements, a double effect evaporator mounted on the frame and consisting of avertically mounted cylindrical shell, a diametrical wall within the shell dividing the shell into a first effect evaporating chamber and a second effect evaporating chamber and a hinged- 9 1y mounted door on each side of the diametrical wall, one for each evaporating chamber and each door carrying a set of tubes which in the closed position of the doors extend into the respective chambers, a steam connection extending to the inlet to the tubes extending into the first effect evaporating chamber of the double effect evaporator, a combined after-condenser and feed water heater mounted vertically adjacent the double effect evaporator and consisting of a cylindrical shell having a coil therein, a connection between the outlet of the tubes extending into the first effect chamber of the double effect evaporator and the shell of the said combined after-condenser and feed water heater, an outlet connection from the shell of the said combined after-condenser and feed water heater, a connection for delivering steam directly to the shell of the said after-condenser and feed water heater, means in said last mentioned connection for controlling the flow of steam to the shell of the said combined after-condenser and feed water heater, control means for said last mentioned means actuated in accordance with the temperature of the water leaving the coil of the said after-condenser and feed water heater, a condenser including a cylindrical shell mounted adjacent said double eifect evaporator and having two separate coils therein, a connection for delivering water to be distilled to the inlet of one of the coils in said condenser, a connection from the outlet of said last mentioned coil to the inlet of the other coil in the condenser, a vapor feed Water heater including a cylindrical shell mounted vertically adjacent the said double effect evaporator and a coil within the shell, a connection between the outlet of said second mentioned coil of the said condenser and the inlet to the coil of said vapor feed water heater, a connection between the outlet of the coil of said vapor feed water heater and the inlet of the coil of the said after-condenser and feed water heater, a connection between the outlet of the coil of the said after-condenser and feed water heater and the first eifect chamber of the said double effect evaporator, a connection between the first effect chamber of said double effect evaporator and the inlet to the tubes extending into said second effect chamber of the double eifect evaporator, a connection between the first effect chamber of said double effect evaporator and the shell of the said vapor feed water heater, and connections connecting the outlet of the coil extending into the second effect chamber of the double effect evaporator, the second effect chamber of the double effect evaporator and the shell of the said vapor feed water heater to the shell of the condenser.

5. In apparatus for evaporating and distilling liquids, a unitary structure comprising base frame and supporting elements, a double effect evaporator mounted on the frame and consisting of a vertically mounted cylindrical shell, a diametrical wall within the shell dividing the shell into a first effect evaporating chamber and a second effect evaporating chamber and a, hingedly mounted door on each side of the diametrical wall, one for each evaporating chamber and each door carrying a set of tubes which in the closed position of the doors extend into the respective chambers, a steam connection extending to the inlet to the tubes extending into the first eifect evaporating chamber of the double 10 effect evaporator, a combined after-condenser and feed water heater mounted vertically adjacent the double effect evaporator and consisting of a cylindrical shell having a coil therein, a connection between the outlet of the tubes extending into the first effect chamber of the double effect evaporator and the shell of the said combined after-condenser and feed water heater, an outlet connection from the shell of the said combined after-condenser and feed Water heater, a connection for delivering steam directly to the shell of the said after-condenser and feed water heater, means in said last mentioned connection for controlling the flow of steam to the shell of the said combined after-condenser and feed water heater, control means for said last mentioned means actuated in accordance with the temperature of the water leaving the coil of the said after-condenser and feed water heater, a condenser including a cylindrical shell mounted adjacent said double effect evaporator and having two separate coils therein, a connection for delivering water to be distilled to the inlet of one of the coils in said condenser, a connection from the outlet of said last mentioned coil to the inlet of the other coil in the condenser, a vapor feed water heater including a cylindrical shell mounted vertically adjacent the said double effect evaporator and a coil within the shell, a connection between the outlet of said second mentioned coil of the said condenser and the inlet to the coil of said vapor feed water heater, a connection between the outlet of the coil of said vapor feed water heater and the inlet of the coil of the said after-condenser and feed water heater, a connection between the outlet of the coil of the said after-condenser and feed water heater and the first effect chamber of the said double effect evaporator, a connection between the first effect chamber of said double effect evaporator and the inlet to the tubes extending into said second effect chamber of the double effect evaporator, a connection between the first effect chamber of said double eifect evaporator and the shell of the said vapor feed water heater, connections connecting the outlet of the coil extending into the second effect chamber of the double effect evaporator, the second effect chamber of the double eifect evaporator and the shell of said vapor feed water heater to the shell of the condenser, open blow-down connections to the chambers of the evaporators, and level controls for controlling the level of the water in the chambers of the double efiect evaporators.

WILLIAM H. THOMPSON.

REFERENCES CITED The following references are of record in the file of this patent: 

